|Publication number||US5090431 A|
|Application number||US 07/531,937|
|Publication date||Feb 25, 1992|
|Filing date||Jun 1, 1990|
|Priority date||Jun 1, 1990|
|Also published as||WO1991018685A1|
|Publication number||07531937, 531937, US 5090431 A, US 5090431A, US-A-5090431, US5090431 A, US5090431A|
|Inventors||Robert L. Theroux, Fatemeh Abnoosi|
|Original Assignee||K & M Electronics, Inc.|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (23), Non-Patent Citations (2), Referenced by (8), Classifications (9), Legal Events (4)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This invention relates to cleaning apparatus, with vapor containment, for use when highly volatile and environmentally hazardous, and also non-environmentally hazardous materials are used as cleaning solvent, e.g., in removing flux from circuit board components and the like.
In the assembly of printed circuit boards, individual components are generally soldered into place using a tin-lead solder and a rosin flux. Following this operation, the assembled board is cleaned to remove all flux. Cleaning solvents in use today which are most efficient for such cleaning are environmentally hazardous. Chlorofluorocarbons and hydrochlorofluorocarbon may be used, the preferred substance being a FREON™. FREON™ is an essentially stable, inert, non-flammable, non-explosive, and non-corrosive fluorocarbon product. In actual use, assembled circuit boards are typically lowered into liquid fluorocarbon or fluorocarbon vapor to effect cleaning.
Present systems for cleaning circuit boards are large, open cleaning tanks which have a basin of liquid cleaning agent, such as FREON™. Conventional gas type refrigeration techniques are used to condense the vapor in order to prevent evaporation. A user places components to be cleaned into a carrier basket, which is then lowered into the vapor layer. All flux dissolves in the vapor and/or liquid, and is filtered out. In some present systems, filtered cleaning agent is recirculated and reused. To reduce the amount of vapor released to the environment by the open tanks of the prior art, users must slowly lower and raise the baskets. A typical rate is 11 inches per minute maximum. The vapor escape problem is compounded by vapor layer non-uniformities which occur in large cleaning tanks, i.e., the central region does not readily form and maintain a uniform vapor layer, primarily due to peripheral location of the heat pumps.
In addition to the environmental problems created by commercially available cleaning tanks, use of such tanks causes disruption in the production line. Due to the large size of the tanks, they are generally centrally located in a production facility. Thus, workers must leave work stations to walk over to the large tank. The slow rate at which components must be lowered into and raised out of the tank makes the entire cleaning process slow, resulting in the loss of valuable labor time. To avoid this loss of labor time, beakers of cleaning solvent are often placed at each work station. There are obvious disadvantages to such an arrangement, including vapor loss to the environment, and potential spills in the work environment. Thus, there is a need for an efficient, bench-top cleaning apparatus for use at a work station.
Accordingly, it is an object of the present invention to provide an improved cleaning apparatus with vapor containment.
It is another object of the invention to provide an efficient, environmentally safe bench-top cleaning apparatus for use in cleaning circuit boards.
These and other objects of the invention are accomplished by an improved cleaning apparatus with vapor containment for use when highly volatile and environmentally hazardous materials are used as cleaning solvent, e.g., in removing flux from circuit boards and the like.
The present invention is a cleaning apparatus having a container for holding a quantity of cleaning agent, which is vaporized and condensed to form an upper vapor layer. Essentially, the container is divided into a lower chamber, for holding the cleaning agent, and an upper chamber for containing the vapors. The chamber may be open to the environment at the top, for enabling introduction of the object to be cleaned, but without vapor escape.
The container of the invention maintains a relatively high temperature in the bottom portion, to vaporize the cleaning agent. One or more heat pumps are adapted to establish a relatively low temperature in the upper region to condense the vapors released by the lower heating process. Conducting metal bands may extend around the upper portion to evenly establish the low temperature. Multiple high thermally conductive shunting devices are coupled between the high temperature end of the heat pumps and the bottom portion of the container to transfer extracted heat from the upper portion to the lower portion, to augment the vaporization process.
Thus, the apparatus of the invention may include one or more heat pumps at the upper portion of the container to form the condensate of the upper vapor layer, while extracted heat from the upper heat pump provides sufficient heat to the lower portion of the container to vaporize the cleaning agent. An additional heat pump may be positioned near the lower portion to heat the cleaning agent.
Sidewall portions of the container may be made from low thermally conductive material and may include at least one layer of insulating material. The heat pumps may be solid state heat pumps for efficiency and economy.
For a fuller understanding of the features, advantages, and objects of the invention, reference should be made to the following detailed description and the accompanying drawings, in which:
FIG. 1 is a perspective view of an embodiment of the apparatus of the present invention.
FIG. 1A is a schematic cut-away view of the embodiment of FIG. 1.
FIG. 2 is a schematic cut-away view of an alternate embodiment of the invention.
FIGS. 1 and 1A show perspective and cut-away views, respectively, of an embodiment of the invention. The overall dimensions of the apparatus are such that it may be positioned at a work station, or on a workbench adjacent to a work area. In the preferred embodiment, the dimensions are 4 inches wide, 5 inches long, and 8 inches high. At this scale, solid state components may economically be utilized. For example, solid state heat pumps may be employed as both the heating and cooling elements.
As shown in FIG. 1A, the apparatus 10 of the invention is a container having a lower vaporizing portion 20 and an adjacent upper condensing portion 30. The lower portion 20 may include a separate solvent containing portion 24 in which a cleaning agent, such as FREON™, may be placed. An optional heating element 22 may be positioned adjacent to the solvent containing portion 24 to invoke vaporization. As the solvent is heated, vapors rise into the upper condensing portion 30 in which they encounter a relatively cold temperature front. The relatively cold temperature may be achieved by means of a cooling element 32, such as a solid state heat pump, having its cool end in good thermal contact with the regions. The container may be open at the top, or have a replaceable top cover (not shown).
The container of the apparatus 10 may consist of multiple alternating layers of insulating material and conductive material. In the illustrated embodiment, the apparatus has outer walls 18, thermal insulation 16, and inner walls 14. Between the outer walls 18 and insulation 16, thermally conductive heat sink straps 40 are positioned for shunting extracted heat from the hot end of upper heat pump 32 to the lower vaporizing portion 20. Thus, one embodiment of the apparatus, wherein element 22 is a high thermally conductive material, may rely solely upon one heat pump located adjacent to the upper portion 30, to provide both the relatively cool upper portion temperature for condensing vapor, and the relatively hot lower portion 20 temperature for vaporizing a cleaning agent. Alternatively, element 22 may be a hot plate or heating element placed adjacent to the lower portion 20 to bring the cleaning agent up to an initial vaporization temperature, after which point the heating element may be thermostatically turned off, and remaining heat may be shunted from the cooling element 32.
In the present embodiment, the apparatus 10 further includes a thermally conductive cooling band 12 around the circumference of the upper portion of the container adjacent to the cooling element 32. The cooling band 12 acts as a conductive material, so that heat is uniformly extracted by the cooling element 32 about the upper portion 30. In this manner, the stratification problem encountered by large units may be alleviated, and a relatively even distribution of condensed vapors may be established across the entire surface of the upper condensation portion 30.
One problem encountered in large units is achieving vapor formation in the center of the condensation layer. An alternate form of the invention is shown, in part, in FIG. 2, including the upper and lower portions 20 and 30, together with the walls defining those portions. To assist with the stratification of condensed vapors, the inner wall of the cooling band 12 may have inwardly extending ridges 60, as shown in FIG. 2. Alternatively, or in conjunction with the ridges 60, the inner walls 14 may angle inward to form lips 34 which protrude into the bottom of the upper portion 30. The lips 34 serve a similar function to the ridges 60.
In one form of the invention, as shown in FIG. 1, the housing for the container 10 may further include multiple sets of louvres and an associated air flow path. In the illustrated embodiment, there are opposing sets of air input louvres 54 associated with the upper portion 30 of the container. Complimentary air output louvres 56 are then positioned near the bottom of the apparatus 10 to enable the circulation of air within the outer container walls 18. The louvres act as cooling means to prevent the heating and cooling elements from overheating. Alternatively, auxiliary fans (not shown) may be positioned about the container to serve a similar general cooling function. The type of cool-down arrangement used will be dependent upon the type of heating and cooling elements utilized. In the illustrated embodiment, solid state heat pumps are used as both the heating element 22 and the cooling element 32, with a louvre assembly providing the general cooling function.
Once the circuit board, or other element, is cleaned, the waste falls to the bottom of the container. In the illustrated embodiment, a stainless steel screen 46 is included to trap and filter the discarded waste. The screen may be periodically removed for cleaning. A tank drain (not shown) may be included at the base of the container for removal of dirty cleaning agent. The drain may lead to a filter unit which traps the waste material and enables the recirculation of cleaning agent.
The cooling band 12 may be manufactured from a metal, such as aluminum or stainless steel. Copper is the preferred metal for conducting energy, however it may be adversely affected by certain cleaning agents. Thus, copper may be plated with nickel, or other protective plating material, to preserve its conductive properties while protecting it from corrosion caused by the cleaning agent being used.
The outer container walls 18 may be manufactured from a non-conductive material. In the preferred embodiment, the outer walls are manufactured from ceramic plates, moldable ceramic, or a non-corrosive plastic. The inner wall may be manufactured from a low thermally conductive solvent-resistant material. In one aspect, solder or thermally conductive flexible epoxy may be used on all faces of the solid state heating element. Thermal grease may be applied to at least one face of each of the lower heating elements for stress, or shear, relief.
Also shown in FIG. 1 are temperature regulators 50, enabling an operator to manually control the temperature of both the optional lower heating element 22 and the upper cooling element 32. Feedback displays 52 may be included to provide important temperature monitoring of the upper and lower portions of the tank. While temperatures in the respective portions are relative, it is an important aspect of the invention that the temperature at the upper portion 30 remains low relative to the temperature of the lower portion 20. This assures that a vapor layer is maintained in the upper portion 30. For example, using FREON™ as the cleaning agent, optimal temperatures for the upper portion are in the range of from about 37°-45° F., and optimal temperature for the lower portion is above 104° F., or above the boiling point of the agent. The range in temperatures between the two container portions assures that a temperature differential will be maintained, even if there is fluctuation from the heating/cooling elements.
The invention can be embodied in other specific forms without departing from the spirit or essential characteristics thereof. The described embodiments of the invention are to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2366949 *||Jan 29, 1943||Jan 9, 1945||Curtiss Wright Corp||Degreasing apparatus|
|US3091098 *||May 4, 1961||May 28, 1963||Pfaudler Permutit Inc||Vacuum deaerator|
|US3308839 *||Oct 12, 1964||Mar 14, 1967||Barday Donald J||Method and apparatus for cleaning objects with solvent|
|US3699006 *||Aug 14, 1970||Oct 17, 1972||James G Hasslacher||Vacuum still having heat exchange coils and particle means therewith|
|US4137929 *||Jul 29, 1977||Feb 6, 1979||Grossman Peter J||Fingernail cleaner|
|US4154003 *||Jun 18, 1976||May 15, 1979||August Lepper, Maschinen-und Apparatebau GmbH||Combined drum washer and drying arrangement|
|US4267022 *||Apr 26, 1978||May 12, 1981||Pitcher Frederick L||Energy efficient process and apparatus for desalinizing water|
|US4308106 *||Aug 1, 1980||Dec 29, 1981||Mannfeld Robert L||Process for removing substantially all water from an alcohol-containing solution for use as a motor fuel or motor fuel additive|
|US4313311 *||Jun 4, 1979||Feb 2, 1982||Mccord James W||Vapor generating and recovering apparatus|
|US4345971 *||Mar 13, 1980||Aug 24, 1982||Watson W Keith R||Distillation employing heat pump|
|US4390396 *||Apr 22, 1981||Jun 28, 1983||Langbein-Pfanhauser Werke Ag||Apparatus for the distillation of vaporizable liquids|
|US4402795 *||Sep 18, 1980||Sep 6, 1983||Erickson Donald C||Reverse absorption heat pump augmented distillation process|
|US4444576 *||Nov 1, 1982||Apr 24, 1984||Koch Process Systems, Inc.||Energy-saving distillative separation using low-temperature heat input|
|US4499743 *||Sep 29, 1983||Feb 19, 1985||Maestrelli S.P.A.||Clothing drycleaning machine|
|US4512814 *||Nov 2, 1983||Apr 23, 1985||Buck James C||Brush conditioner for car wash|
|US4532983 *||Jun 6, 1983||Aug 6, 1985||Haden Schweitzer Corporation||Water curtain apparatus for heat energy recovery from escaping steam|
|US4556457 *||Dec 27, 1982||Dec 3, 1985||Mccord James W||Safety control device for vapor generating and recovering apparatus|
|US4626321 *||Feb 13, 1986||Dec 2, 1986||Trustees Of Dartmouth College||Distillation systems and methods|
|US4645569 *||Nov 22, 1983||Feb 24, 1987||Shinnenryoyu Kaihatsugijutsu Kenkyukumiai||Process for producing anhydrous ethanol|
|US4690158 *||Jan 29, 1985||Sep 1, 1987||Daiwa Special Chemical Co., Ltd.||Washing apparatus|
|US4695349 *||Mar 7, 1985||Sep 22, 1987||Linde Aktiengesellschaft||Process and apparatus for distillation and/or stripping|
|US4755261 *||Jan 2, 1987||Jul 5, 1988||Mccord James W||Vapor generating and recovery method for vapor retention and reuse|
|US4757831 *||Jan 30, 1987||Jul 19, 1988||Century International Corp.||Golf club cleaning machine|
|1||*||Cole Parmer Instrument Company 1989 1990 Catalog, Chicago, Il.|
|2||Cole-Parmer Instrument Company 1989-1990 Catalog, Chicago, Il.|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US5320756 *||Jun 29, 1993||Jun 14, 1994||Church & Dwight Co., Inc.||Method of treating aqueous alkaline effluents derived from cleaning electronic circuit assemblies|
|US5320758 *||Jun 29, 1993||Jun 14, 1994||Church & Dwight Co., Inc.||Method of recycling amine saponifiers used in cleaning electronic circuit boards|
|US8112903 *||Feb 8, 2007||Feb 14, 2012||Electrolux Home Products Corporation N.V.||Household clothes drying machine with additional condenser|
|US20080025869 *||Aug 7, 2007||Jan 31, 2008||Kendall Richard J||Sterilization system and method with heat pump operated vaporizer/condenser|
|US20090152093 *||Nov 29, 2005||Jun 18, 2009||Frederick William Millar||Liquid treatment device and method|
|US20100139111 *||Feb 8, 2007||Jun 10, 2010||Ugo Favret||Household Clohtes Drying Machine with Additonal Condesner|
|US20110155556 *||Feb 4, 2011||Jun 30, 2011||Aquamill Five Star Pty Ltd||Liquid treatment device and method|
|WO2007073050A1 *||Dec 11, 2006||Jun 28, 2007||Byoung-Goan Park||Thermoelectrical work plate|
|U.S. Classification||134/105, 203/DIG.5, 134/184, 134/182, 134/200|
|Cooperative Classification||Y10S203/05, C23G5/04|
|Jun 1, 1990||AS||Assignment|
Owner name: K AND M ELECTRONICS, INC., A CORP. OF MA., MASSACH
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:THEROUX, ROBERT L.;ABNOOSI, FATEMEH;REEL/FRAME:005329/0410
Effective date: 19900530
|Oct 3, 1995||REMI||Maintenance fee reminder mailed|
|Feb 25, 1996||LAPS||Lapse for failure to pay maintenance fees|
|May 7, 1996||FP||Expired due to failure to pay maintenance fee|
Effective date: 19960228